U.S. patent application number 12/361264 was filed with the patent office on 2009-07-30 for microreactor assembly incorporating interconnect backbone and diverse fluidic microstructures.
Invention is credited to Jean-Pierre Henri Rene Lereboullet, Olivier Lobet, Yann P. M. Nedelec, Ronan Tanguy.
Application Number | 20090191102 12/361264 |
Document ID | / |
Family ID | 39345289 |
Filed Date | 2009-07-30 |
United States Patent
Application |
20090191102 |
Kind Code |
A1 |
Lereboullet; Jean-Pierre Henri Rene
; et al. |
July 30, 2009 |
MICROREACTOR ASSEMBLY INCORPORATING INTERCONNECT BACKBONE AND
DIVERSE FLUIDIC MICROSTRUCTURES
Abstract
A microreactor assembly [100] is provided comprising a fluidic
interconnect backbone [10] and plurality of fluidic
microstructures. Interconnect input/output ports [12] of the
fluidic interconnect backbone [10] are interfaced with microchannel
input/output ports [14] of the fluidic microstructures at a
plurality of non-polymeric interconnect seals [50]. Interconnect
microchannels [15] are defined entirely by the fluidic interconnect
backbone [10] and extend between the non-polymeric interconnect
seals [50] without interruption by additional sealed interfaces. At
least one of the fluidic microstractures [20, 30, 40] may comprise
a mixing microstructure formed by a molding process. Another of the
fluidic microstructures [20, 30, 40] may comprise an extruded
reactor body. Still another fluidic microstructure [20, 30, 40] may
comprise a quench-flow or hydrolysis microreactor formed by a
hot-pressing method.
Inventors: |
Lereboullet; Jean-Pierre Henri
Rene; (Bois le Roi, FR) ; Lobet; Olivier;
(Mennecy, FR) ; Nedelec; Yann P. M.; (Avon,
FR) ; Tanguy; Ronan; (Grez Sur Loing, FR) |
Correspondence
Address: |
CORNING INCORPORATED
SP-TI-3-1
CORNING
NY
14831
US
|
Family ID: |
39345289 |
Appl. No.: |
12/361264 |
Filed: |
January 28, 2009 |
Current U.S.
Class: |
422/162 ;
264/605; 264/607; 422/129; 422/198; 422/240 |
Current CPC
Class: |
B01J 2219/0081 20130101;
B01L 2300/185 20130101; B01J 2219/00873 20130101; C04B 2237/32
20130101; B01J 2219/00783 20130101; B01J 2219/00804 20130101; B01J
2219/00891 20130101; B01L 3/565 20130101; B01J 2219/0086 20130101;
B01L 2200/0689 20130101; B01L 3/502707 20130101; B01J 2219/00824
20130101; B01L 2300/0816 20130101; B01L 3/502715 20130101; C04B
37/005 20130101; C04B 2237/10 20130101; B01L 2200/028 20130101;
B01J 19/0093 20130101; B01J 2219/00889 20130101; B01L 2300/0874
20130101; B01J 2219/00831 20130101; C04B 37/045 20130101; B01L
2200/027 20130101 |
Class at
Publication: |
422/162 ;
422/129; 422/198; 422/240; 264/605; 264/607 |
International
Class: |
B01J 19/00 20060101
B01J019/00; C04B 35/64 20060101 C04B035/64 |
Foreign Application Data
Date |
Code |
Application Number |
Jan 30, 2008 |
EP |
08305011.2 |
Claims
1. A microreactor assembly [100] comprising a fluidic interconnect
backbone [10] and plurality of fluidic microstructures [20, 30,
40], wherein: each of the fluidic microstructures [20, 30, 40]
comprises a plurality of fluidic microchannels comprising
respective microchannel input/output ports [14]; the fluidic
interconnect backbone [10] comprises at least one interconnect
microchannel [15] comprising interconnect input/output ports [12];
the microreactor assembly [100] comprises a plurality of
non-polymeric interconnect seals [50] associated with the
interconnect input and output ports [12]; interconnect input/output
ports [12] of the fluidic interconnect backbone [10] are interfaced
with microchannel input/output ports [14] of the fluidic
microstructures [20, 30, 40] at one of the non-polymeric
interconnect seals [50]; and the interconnect microchannel [15] is
defined entirely by the fluidic interconnect backbone [10] and is
configured such that it extends between the non-polymeric
interconnect seals [50] without interruption by additional sealed
interfaces.
2. A microreactor assembly as claimed in claim 1 wherein: at least
one of the plurality of fluidic microstructures comprises a mixing
microstructure formed by a molding process; at least one of the
plurality of fluidic microstructures comprises an extruded reactor
body; and at least one of the plurality of fluidic microstructures
comprises a quench-flow or hydrolysis microreactor formed by a
hot-pressing method.
3. A microreactor assembly as claimed in claim 1 wherein: the
plurality of fluidic microstructures define a diverse fluidic
microstructure set comprising respective microstructure
configurations that represent a plurality of different
manufacturing processes; the respective configurations of the
interconnect input/output ports of the interconnect backbone are
substantially identical; and the non-polymeric interconnect seals
are configured to interface the substantially identical
interconnect input/output ports with corresponding microchannel
input/output ports of the diverse fluidic microstructure set.
4. A microreactor assembly as claimed in claim 3 wherein the
plurality of different manufacturing processes comprise injection
molding, flat molding, hot pressing, extrusion, and combinations
thereof.
5. A microreactor assembly as claimed in claim 1 wherein: the
plurality of fluidic microstructures define a diverse microreactor
functionality set comprising a plurality of different microreactor
functions; the respective configurations of the interconnect
input/output ports of the interconnect backbone are substantially
identical; and the non-polymeric interconnect seals are configured
to interface the substantially identical interconnect input/output
ports with corresponding microchannel input/output ports of the
diverse fluidic microstructure set.
6. A microreactor assembly as claimed in claim 5 wherein the
plurality of different microreactor functions comprise fluid
distribution, thermal exchange, reactant mixing, quench-flow,
hydrolysis, residence time, and combinations thereof.
7. A microreactor assembly as claimed in claim 1 wherein: the
plurality of fluidic microstructures define a diverse microreactor
structure set comprising a plurality of different structural
configurations; the respective configurations of the interconnect
input/output ports of the interconnect backbone are substantially
identical; and the non-polymeric interconnect seals are configured
to interface the substantially identical interconnect input/output
ports with corresponding microchannel input/output ports of the
diverse microreactor structure set.
8. A microreactor assembly as claimed in claim 7 wherein the
plurality of different structural configurations comprise a fluid
distribution microstructure, a thermal exchange microstructure, a
reactant mixing microstructure, a quench-flow microstructure, a
hydrolysis microstructure, and combinations thereof.
9. A microreactor assembly as claimed in claim 1 wherein: the
plurality of fluidic microstructures define a diverse fluidic
microstructure set comprising respective microstructure
configurations that represent a plurality of different
manufacturing processes; each of the plurality of different
manufacturing processes comprises a common sintering step; and the
non-polymeric interconnect seals are configured to interface the
substantially identical interconnect input/output ports with
corresponding microchannel input/output ports of the diverse
fluidic microstructure set upon execution of the common sintering
step.
10. A microreactor assembly as claimed in claim 1 wherein the
non-polymeric interconnect seals comprise sintered glass portions
of the fluidic interconnect backbone and the fluidic
microstructures.
11. A microreactor assembly as claimed in claim 1 wherein the
non-polymeric interconnect seals comprise a layer of sintered glass
particles interposed between adjacent glass portions of the fluidic
interconnect backbone and the fluidic microstructures.
12. A microreactor assembly as claimed in claim 11 wherein the
sintered glass particles exhibit a coefficient of thermal
elongation that is compatible with the coefficient of thermal
elongation of the adjacent glass portions of the fluidic
interconnect backbone and the fluidic microstructures.
13. A microreactor assembly as claimed in claim 11 wherein the
layer of sintered glass particles is derived from a paste
comprising the sintered glass particles and a binder.
14. A microreactor assembly as claimed in claim 1 wherein the
non-polymeric interconnect seals comprise a sealed interface formed
jointly by a glass portion of one of the fluidic microstructures, a
glass portion of the fluidic interconnect backbone, and an
intervening non-polymeric bonding material.
15. A microreactor assembly as claimed in claim 1 wherein the
non-polymeric interconnect seals comprise a sealed interface formed
jointly by a glass or ceramic portion of one of the fluidic
microstructures, a glass or ceramic portion of the fluidic
interconnect backbone, and an intervening non-polymeric bonding
material.
16. A microreactor assembly as claimed in claim 1 wherein the
non-polymeric interconnect seals comprises a glass/ceramic sealed
interface formed from a glass portion of either the fluidic
interconnect backbone or the fluidic microstructures and a ceramic
portion of either the fluidic interconnect backbone or the fluidic
microstructures.
17. A microreactor assembly as claimed in claim 1 wherein the
non-polymeric interconnect seals comprise a sealed interface formed
jointly by a ceramic portion of one of the fluidic microstructures
and a ceramic portion of the fluidic interconnect backbone.
18. A microreactor assembly as claimed in claim 1 wherein the
fluidic interconnect backbone and the plurality of fluidic
microstructures are configured such that a selected plurality of
the fluidic microstructures define a support plane along which the
fluidic microstructures and the interconnect backbone of the
microreactor assembly can be supported.
19. A microreactor assembly as claimed in claim 18 wherein: the
fluidic microstructures defining the support plane are positioned
on one face of the interconnect backbone; and remaining fluidic
microstructures of the microreactor assembly are positioned on
another face of the interconnect backbone.
20. A microreactor assembly as claimed in claim 19 wherein: the
fluidic microstructures positioned on both faces of the
interconnect backbone comprise respective microstructure
configurations that represent a plurality of different
manufacturing processes with a common sintering step; and the
non-polymeric interconnect seals are configured to interface the
interconnect input/output ports with corresponding microchannel
input/output ports of the fluidic microstructures upon execution of
the common sintering step, when the interconnect backbone and the
fluidic microstructures are supported along the support plane
defined by the selected plurality of the fluidic
microstructures.
21. A microreactor assembly as claimed in claim 1 wherein the
fluidic microstructures comprise stacked fluidic microstructures
supported by a common face of the interconnect backbone.
22. A microreactor assembly as claimed in claim 1 wherein the
fluidic microstructures comprise at least one opposite-side
interconnecting fluidic microstructure configured to place two
fluidic microstructures in fluid communication with each other.
23. A method of fabricating a microreactor assembly comprising a
fluidic interconnect backbone and plurality of fluidic
microstructures, wherein each of the fluidic microstructures
comprises a plurality of fluidic microchannels comprising
respective microchannel input/output ports, the fluidic
interconnect backbone comprises at least one interconnect
microchannel comprises interconnect input/output ports, and the
method comprises: aligning the fluidic interconnect backbone and
the fluidic microstructures by aligning the microchannel
input/output ports with the interconnect input/output ports; and
sintering the interconnect backbone and fluidic microstructure in
the aligned state to form a plurality of non-polymeric interconnect
seals associated with the interconnect input and output ports such
that the interconnect input/output ports of the fluidic
interconnect backbone are interfaced with microchannel input/output
ports of the fluidic microstructures at one of the non-polymeric
interconnect seals.
24. A method as claimed in claim 23 wherein the interconnect
backbone and the fluidic microstructures are supported by a
sintering support plate in a support plane defined a plurality of
the fluidic microstructures during sintering.
25. A method as claimed in claim 24 wherein the interconnect
backbone and the fluidic microstructures are supported by the
sintering support plate in a state of assembly where components of
the fluidic microstructures are in an un-sintered green state.
Description
PRIORITY
[0001] This application claims priority to European Patent
Application number 08305011.2, filed Jan. 30, 2008, titled
"Microreactor Assembly Incorporating Interconnect Backbone and
Diverse Fluidic Microstructures".
BACKGROUND
[0002] The present invention relates to microreactor technology.
Microreactors are commonly referred to as microstructured reactors,
microchannel reactors, or microfluidic devices. Regardless of the
particular nomenclature utilized, the microreactor is a device in
which a moving or static target sample is confined and subject to
processing. In some cases, the processing involves the analysis of
chemical reactions. In others, the processing is executed as part
of a manufacturing process utilizing two distinct reactants. In
still others, a moving or static target sample is confined in a
microreactor as heat is exchanged between the sample and an
associated heat exchange fluid. In any case, the dimensions of the
confined spaces are generally on the order of about 1 mm.
Microchannels are the most typical form of such confinement and the
microreactor is usually a continuous flow reactor, as opposed to a
batch reactor. The reduced internal dimensions of the microchannels
provide considerable improvement in mass and heat transfer rates.
In addition, microreactors offer many advantages over conventional
scale reactors, including vast improvements in energy efficiency,
reaction speed, reaction yield, safety, reliability, scalability,
etc.
[0003] Microreactors often comprise plural distinct fluidic
microstructures that are in fluid communication with each other and
are configured to execute different functions in the microreactor.
For example, and not by way of limitation, an initial
microstructure may be configured to mix two reactants. Subsequent
microstructures may be configured for heat exchange, quenching,
hydrolysis, etc, or simply to provide a controlled residence time
for the mixed reactants. The various distinct microstructures must
often be placed in serial or parallel fluid communication with each
other. In many cases, the associated components for directing the
reactants to the proper microchannels within the network can be
fairly complex. Further, the components need to be configured for
operation under high temperatures and pressures. As a result,
microreactor configurations such as that disclosed in published
international patent application WO-2007-036513 employ a variety of
fluidic ducts, fittings, adapters, O-rings, screws, clamps, and
other types of connection elements to interconnect various
microstructures within the microreactor configuration. Each
individual elements increases the complexity of the system and is a
potential source of leakage or other error within the system. The
present invention relates generally to the design of a microreactor
assembly that reduces the use of many of the aforementioned
connection elements and provides a common fluid communication
platform upon which a variety of distinct microreactor structures
can be supported and placed in fluid communication with each
other.
[0004] According to one embodiment of the present invention, a
microreactor assembly is provided comprising a fluidic interconnect
backbone and plurality of fluidic microstructures. Interconnect
input/output ports of the fluidic interconnect backbone are
interfaced with microchannel input/output ports of the fluidic
microstructures at a plurality of non-polymeric interconnect seals.
Interconnect microchannels are defined entirely by the fluidic
interconnect backbone and extend between the non-polymeric
interconnect seals without interruption by additional sealed
interfaces. At least one of the fluidic microstructures may
comprise a mixing microstructure formed by a molding process.
Another of the fluidic microstructures may comprise an extruded
reactor body. Still another fluidic microstructure may comprise a
quench-flow or hydrolysis microreactor formed by a hot-pressing
method.
BRIEF DESCRIPTION OF THE FIGURES
[0005] The following detailed description of specific embodiments
of the present invention can be best understood when read in
conjunction with the following drawings, where like structure is
indicated with like reference numerals and in which:
[0006] FIG. 1 is a schematic illustration of a microreactor
assembly according to one embodiment of the present invention;
[0007] FIGS. 1A and 1B illustrate alternative configurations of
portions of the microreactor assembly including non-polymeric
interconnect seals;
[0008] FIGS. 2-4 are schematic illustrations of microreactor
assemblies according to additional embodiments of the present
invention; and
[0009] FIGS. 5-7 illustrate particular aspects of minireactor
structures suitable for use in microreactor assemblies according to
the present invention.
DETAILED DESCRIPTION
[0010] Referring to FIG. 1, a microreactor assembly 100 according
to one embodiment of the present invention is illustrated.
Generally, the microreactor assembly 100 comprises a fluidic
interconnect backbone 10 and plurality of fluidic microstructures
20, 30, 40. The fluidic interconnect backbone 10 comprises a number
of interconnect microchannels 15, each of which comprises
interconnect input/output ports 12. Similarly, each of the fluidic
microstructures 20, 30, 40 comprises a plurality of fluidic
microchannels and respective microchannel input/output ports
14.
[0011] Although the present invention is not limited to the use of
a specific microreactor configuration or the use of specific
microstructures, in the illustrated embodiment, the first
microstructure 20 can be configured to mix two reactants and to
provide for heat exchange between the reactants and a thermal
fluid. To these ends, it is noted that first microstructure 20 will
typically comprise fluidic microchannels that are configured to
distribute the reactants across a plurality of reactant flow paths.
Each of these reactant flow paths would then be subsequently
directed to a mixing zone within the first microstructure 20 where
the reactants mix and react. In addition, the first microstructure
20 may also comprise thermal fluid microchannels configured for
thermal exchange between a reactant fluid in the fluidic
microchannels and a thermal fluid in the thermal fluid
microchannels. Alternatively, the first microstructure 20 may
merely be configured as a single function microstructure, i.e., as
a fluid distribution microstructure, a thermal exchange
mictrostructure, or a reactant mixing microstructure. The specific
design of the fluidic microstructure for any combination of these
functions can be gleaned from a variety of teachings in the art,
including those present in Coming Incorporated European Patent
Applications EP 1 679 115 A1, EP 1 854 536 A1, EP 1 604 733 A1, EP
1 720 650 A0, and other similarly classified European patents and
patent applications.
[0012] The second microstructure 30 is illustrated downstream of
the first microstructure 20 and, in the illustrated embodiment, is
configured primarily as a minireactor configured to provide a large
volume of microchannels extending the residence time of the
reactants therein. Alternatively, or additionally, the second
microstructure 30 may be configured to execute various combinations
of the functions described with reference to the first
microstructure 20, i.e., fluid distribution, thermal exchange,
reactant mixing. Referring to FIGS. 5-7, it is contemplated that
the minireactor 30 can be fabricated as an extruded honeycomb
structure 60, with particular longitudinal passages 62 of the
honeycomb structure 60 designated for the passage of thermal fluids
and reactants, respectively. As is illustrated in FIGS. 6 and 7,
residence time within the honeycomb structure can be enhanced by
capping selected ends 64 of the longitudinal honeycomb passages 62
and removing portions of the honeycomb walls 66 to place adjacent
passages 62 in communication with each other near the capped ends
64 and define a circuitous flow path in the honeycomb structure 60.
The flow paths illustrated in FIGS. 6 and 7 are presented for
illustrative purposes only and, as will be appreciated by those
practicing the present invention, a variety of more complex or less
complex flow paths may be constructed by selecting particular
passages for capping and wall removal.
[0013] The third microstructure 40 is illustrated downstream of the
first and second microstructures in FIG. 1 and, in the illustrated
embodiment, is configured primarily as a relatively large channel
microreactor that is typically used for operations where low
pressure drop and low resistance to flow are important, as would be
the case for multichannel quench-flow or hydrolysis
microreactors.
[0014] Typically, the microstructures 20, 30, 40 will be formed by
two or more distinct manufacturing methods, particularly when the
respective microstructures are configured to execute different
functions, or different combinations of functions. For example, if
the first microstructure 20 is primarily configured for reactant
mixing, it may be formed by various flat molding processes, if the
second microstructure 30 is configured as a minireactor, it can be
formed through extrusion processes, and, if the third
microstructure 40 is configured as a quench-flow or hydrolysis
microreactor, it may be formed by hot-pressing methods, all of
which are documented in the above-referenced applications. Given
this potentially diverse constituency, the various fluidic
interconnect backbones 10 illustrated herein allow those practicing
the present invention to construct common backbone microreactor
assemblies using fluidic microstructures that have been
manufactured under a variety of different protocols that would not
otherwise be amenable to assembly on a common interconnect
backbone.
[0015] To this end, the microreactor assembly 100 is provided with
a plurality of non-polymeric interconnect seals 50 associated with
the interconnect input/output ports 12. More specifically, the
interconnect input/output ports 12 of the fluidic interconnect
backbone 10 are interfaced with microchannel input/output ports 14
of the fluidic microstructures 20, 30, 40 at one of the
non-polymeric interconnect seals 50. The non-polymeric interconnect
seals 50 can be formed in a variety of ways. In one embodiment, the
non-polymeric interconnect seals 50 are formed as adjoining
sintered glass portions of the fluidic interconnect backbone 10 and
the fluidic microstructures 20, 30, 40. Alternatively, referring to
FIGS. 1A and 1B, the non-polymeric interconnect seals 50 may be
formed by providing discrete or continuous layers 52 of sintered
glass particles interposed between adjacent glass portions of the
fluidic interconnect backbone 10 and the fluidic microstructures
20, 30, 40.
[0016] Where a discrete or continuous layer of sintered glass
particles are utilized to form the non-polymeric interconnect seals
50, it may be advantageous to provide sintered glass particles that
exhibit a coefficient of thermal elongation that is compatible with
the coefficient of thermal elongation of the adjacent glass
portions of the fluidic interconnect backbone 10 and the fluidic
microstructures 20, 30, 40. It may also be preferable to provide
the layer of sintered glass particles as a paste comprising the
sintered glass particles and a binder, such as paraffin. In further
alternative embodiments, the non-polymeric interconnect seals 50
comprise a sealed interface formed jointly by a glass or ceramic
portion of one of the fluidic microstructures, a glass or ceramic
portion of the fluidic interconnect backbone, and an intervening
non-polymeric bonding material. In any case, the interconnect seals
50 are selected to be non-polymeric for improved performance at
relatively high or relatively low operating temperatures, i.e.,
temperatures at which polymeric seals would fail or degrade.
[0017] The interconnect microchannels 15 are defined entirely by
the fluidic interconnect backbone and extend between the
non-polymeric interconnect seals 50 without interruption by, for
example, additional sealed interfaces that would otherwise be
presented if tubing, connectors, valves or other fluid handling
hardware were used to couple the fluidic microstructures 20, 30,
40. As illustrated in FIG. 1, each interconnect input/output port
12 of the fluidic interconnect backbone 10 is interfaced with a
corresponding microchannel input/output port 14 of one of the
fluidic microstructures 20, 30, 40 at one of the non-polymeric
interconnect seals 50. As a result, the microreactor assembly 100
utilizes the interconnect backbone 10 to provide a high performance
connection between the fluidic microstructures 20, 30, 40--in terms
of chemical resistance and operating pressure and temperature. The
interconnect backbone 10 also simplifies the microreactor assembly
100 by significantly decreasing the number of external connections
between microstructures and the associated securing and sealing
hardware.
[0018] Further, the interconnect backbone 10 can improve process
control in microreactor assemblies because it can also be
configured to incorporate thermal interconnect microchannels 16.
More specifically, referring collectively to FIGS. 1, 3, and 4, if
any of the fluidic microstructures 20, 30, 40 were to include
thermal fluid microchannels configured for thermal exchange between
a reactant fluid and a thermal fluid moving through adjacent
microchannels of the microstructure, the thermal interconnect
microchannels 16 can be placed in fluid communication with the
thermal fluid microchannels of the fluidic microstructures 20, 30,
40 via additional non-polymeric interconnect seals 50.
[0019] As is illustrated in FIG. 1, the fluidic interconnect
backbone 10 can be configured as a multilayer manifold comprising a
network of cross-layer openings and intra-layer blockages
configured to segregate individual layers of the multilayer
manifold into a plurality of independent interconnect
microchannels. As a result, the fluidic interconnect backbone 10
can be configured to complement a variety of fluidic
microstructures of varying complexity. The respective positions of
the cross-layer openings can be selected such that the interconnect
input and output ports 12 complement standard I/O patterns of a
variety of microfluidic structures or customized I/O patterns for
highly specialized applications. In addition, by constructing the
interconnect backbone 10 of glass, ceramic, or composite materials
that are amenable to modification, the respective size, positions,
and shape of the cross layer openings can be customized to match a
variety of technical applications.
[0020] As is noted above, the fluidic microstructures 20, 30, 40
may define a set of diverse fluidic microstructures representing a
plurality of different manufacturing processes including, for
example, injection molding, flat molding, hot pressing, extrusion,
etc. In this context, the non-polymeric interconnect seals 50 are
able to interface the interconnect input/output ports 12 with
corresponding microchannel input/output ports 14 of the diverse
fluidic microstructures 20, 30, 40, even though the respective
interconnect input/output ports 12 are substantially identical,
i.e., they are formed from the same interconnect backbone 10--a
non-diverse structure. As a result, in practicing the present
invention, the interconnect backbone 10 may be utilized to form
non-polymeric interconnect seals with fluidic microstructures 20,
30, 40 that define a variety of different structural configurations
and microreactor functions including, but not limited to, fluid
distribution, thermal exchange, reactant mixing, quench-flow,
hydrolysis, residence time, and combinations thereof.
[0021] To manufacture microreactor assemblies 100 according to the
present invention, particularly those where the fluidic
microstructures represent a plurality of different manufacturing
processes, it will often be possible to tailor the fabrication
scheme so that each of the plurality of different manufacturing
processes comprise a common sintering step. In this case, the
non-polymeric interconnect seals can be formed upon execution of
the common sintering step. More specifically, given a microreactor
assembly 100 comprising a fluidic interconnect backbone 10 and
plurality of different fluidic microstructures 20, 30, 40, the
fluidic interconnect backbone 10 can first be aligned with the
fluidic microstructures 20, 30, 40 by aligning the microchannel
input/output ports 14 with suitably located interconnect
input/output ports 12. Once aligned, the entire assembly 100 is
sintered in the aligned state to form the non-polymeric
interconnect seals 50 and to complete fabrication of the
un-sintered or "green" portions of the various fluidic
microstructures 20, 30, 40.
[0022] Referring to FIG. 4, to facilitate the aforementioned
universal sintering, the fluidic interconnect backbone 10 and the
fluidic microstructures 20, 30, 40 can be configured such that
selected microstructures define a support plane along which the
microstructures and backbone can be supported. For example, in FIG.
4, a set of fluidic microstructures 40 are positioned on the lower
face of the interconnect backbone 10 to define the support plane.
The remaining fluidic microstructures 20, 30 are positioned on the
upper face of the interconnect backbone 10. Given this
configuration, and configurations similar to it, the interconnect
backbone 10 and the fluidic microstructures 20, 30, 40 can be
supported by a sintering support plate 70 in a state of assembly
where components of the fluidic microstructures are in an
un-sintered green state and, as positioned, can be subject to the
aforementioned sintering step.
[0023] As will be appreciated by those familiar with microreactor
technology, the complexity of the reactant and thermal exchange
microchannels illustrated herein can vary widely and has merely
been illustrated in relatively simple schematic form. For example,
a relatively simple microreactor assembly 100 according to the
present invention is illustrated in FIG. 2, while more complex
assemblies 100 are illustrated in FIGS. 3 and 4. In FIG. 3,
relatively large channel microreactor 40 is used interconnect a
pair of mixing microstructures 20 and respective minireactors 30
are stacked on corresponding mixing microstructures.
[0024] It is noted that recitations herein of a component of the
present invention being "configured" in a particular way, to embody
a particular property, or function in a particular manner, are
structural recitations as opposed to recitations of intended use.
More specifically, the references herein to the manner in which a
component is "configured" denote an existing physical condition of
the component and, as such, are to be taken as a definite
recitation of the structural characteristics of the component.
[0025] For the purposes of describing and defining the present
invention it is noted that the term "substantially" is utilized
herein to represent the inherent degree of uncertainty that may be
attributed to any quantitative comparison, value, measurement, or
other representation.
[0026] Having described the invention in detail and by reference to
specific embodiments thereof, it will be apparent that
modifications and variations are possible without departing from
the scope of the invention defined in the appended claims. More
specifically, although some aspects of the present invention are
identified herein as preferred or particularly advantageous, it is
contemplated that the present invention is not necessarily limited
to these preferred aspects of the invention.
* * * * *